| |
 |
Controlled etching of oxides via gas phase reactions |
| 5439553 |
Controlled etching of oxides via gas phase reactions
|
|
| Patent Drawings: | |
| Inventor: |
Grant, et al. |
| Date Issued: |
August 8, 1995 |
| Application: |
08/219,961 |
| Filed: |
March 30, 1994 |
| Inventors: |
Grant; Robert W. (Allenstown, PA)
Ruzyllo; Jerzy (State College, PA)
Torek; Kevin (State College, PA)
|
| Assignee: |
Penn State Research Foundation (University Park, PA) |
| Primary Examiner: |
Fourson; George |
| Assistant Examiner: |
Bilodeau; Thomas G. |
| Attorney Or Agent: |
Cobrin Gittes & Samuel |
| U.S. Class: |
216/58; 216/79; 257/E21.252 |
| Field Of Search: |
156/646; 156/643; 156/657; 156/345; 156/662 |
| International Class: |
|
| U.S Patent Documents: |
3194703; 3272748; 3592773; 3598741; 3677848; 3813311; 3966517; 4746397; 4749440; 4857142; 4871416; 4921572; 5022961; 5078832; 5112437; 5228206; 5234540 |
| Foreign Patent Documents: |
|
| Other References: |
Bersin, R. L., "The Dry Ox Process for Etching Silicon Dioxide" Solid State Technology, Apr. 1977, pp. 78-80..
Butterbaugh, J. W., Hiatt, C. F. and Gray, D. C.; "Gas-Phase Etching of Silicon Oxide with Anhydrous HF and Isopropanol", Third Int'l Symposium on Cleaning Technology in Semiconductor Development Mfg., Subcommittee of Electrochmemical Society, Oct.15-20, 1993..
Miki, N., Kikuyama, H., Maeno, M. Murota, J., and Ohmi, T.; "Selective Etching of Native Oxide By Dry Processing Using Ultra Clean Anhydrous Hydrogen Fluoride", 1988 IEEE, 730-733..
Jackman, R. B., Ebert, H. and Foord, J. S.; "Reaction Mechanisms For The Photon-Enhanced Etching Of Semiconductors: An Investigation Of The UV-Stimulated Interaction of Chlorine With Si(100)", Surface Science 176 (1986) 183-192..
Miki, N., Kikuyama, H., Kawanabe, I. Miyashita M., and Ohmi T.; "Gas-Phase Selective Etching Of Native Oxide", IEEE 37:1 (1190) 107-115..
Philipossian, A.; "The Activity of HF/H.sub.2 O Treated Silicon Surfaces in Ambient Air Before And After Gate Oxidation", J. Electrochem. Soc., vol. 139, No. 10, Oct. 1992, 2956-2961..
Ito, T., "Wafer Dry Cleaning With Photo-Excited Halogen Radicals", Proceedings--Institute of Environmental Sciences, pp. 808-813, 1991..
Ruzyllo, J., Torek, K., Daffron, C., Grant R., and Novak, R.; "Etching of thermal Oxides in Low Pressure Anhydrous HF/CH.sub.3 OH Gas Mixture at Elevated Temperature", J. Electrochem. Soc., vol. 140, No. 4, Apr. 1993..
Kao, D. B., Cairns, B. R., and Deal, B. E., "Vapor -Phase pre-Cleans for Furnace-Grown and Rapid-Thermal Thin Oxides." in: Ruzyllo, J., Novak, R. E., Proceedings of the Second International Symposium on Cleaning Technology in Semiconductor DeviceManufactoring , the Electrochemical Society Softbound Proceedings Series (Pennington, N.J. 1992), pp. 251-259..
Izumi, A., Matsuka, T., Takeuchi, T. and Yamano, A., "A New Cleaning Method By Using Anhydrous HF/CH.sub.3 OH Vapor System." in: Ruzyllo, J., Novak, R. E., Proceedings of the Second Internatinal Symposium on Cleaning Technology in SemiconductroDevice Manufacturing, the Electrochemical Society Softbound Proceedings Series (Pennington, N.J. 1992), pp. 260-267..
Deal, B. E. and Helms, R., "Vapor Phase Wafer Cleaning Technology", Handbook of Semiconductor Wafer Cleaning Technology, pp. 274-297..
Ruzyllo, J., "Overview of Dry Wafer Cleaning Processes", Chapter 5 in: Handbook of Silicon Wafer Cleaning Technology, pp. 274-297, Noyes Publications, 1993..
Abstract, Toke, 1987 Derwent Publications Ltd.. |
|
| Abstract: |
Oxides are etched with a halide-containing species and a low molecular weight organic molecule having a high vapor pressure at standard conditions, where etching is performed at preset wafer temperature in an enclosed chamber at a pressure such that all species present in the chamber, including water, are in the gas phase and condensation of species present on the etched surface is controlled. Thus all species involved remain in the gas phase even if trace water vapor appears in the process chamber. Preferably, etching is performed in a cluster dry tool apparatus. |
| Claim: |
What is claimed is:
1. A method of etching oxides on a surface of a substrate, said substrate being at a temperature, said method comprising etching with a gas phase mixture of ahalide-containing species, an organic material having a higher vapor pressure than water at standard conditions of room temperature and pressure of 1 atmosphere and water, in an enclosed chamber at a pressure such that water is substantially maintainedin the gas phase and condensation of species present on the etched surface is minimized.
2. A method of etching as claimed in claim 1 where the etching is performed in an enclosed chamber of a cluster dry tool apparatus.
3. A method of etching as claimed in claim 1 where the organic material having a higher vapor pressure than water at standard conditions of room temperature and pressure of 1 atmosphere is selected from the group consisting of alcohols, organicacids, ketones and alkanes.
4. A method of etching as claimed in claim 3 where the organic material having a higher vapor pressure than water at standard conditions of room temperature and pressure of 1 atmosphere is selected from the group consisting of methanol,isopropanol, acetone, acetic acid and methane.
5. A method of etching as claimed in claim 1 where the halide-containing species is selected from the group consisting of HF, NF.sub.3, ClF.sub.3 and F.sub.2.
6. A method of etching as claimed in claim 1 where the halide-containing species is HF, the organic material having a higher vapor pressure than water at standard conditions of room temperature and pressure of 1 atmosphere is methanol, thepressure is 100 Torr and the preset temperature is from 20.degree. C. to 95.degree. C.
7. A method of etching as claimed in claim 1 where the halide-containing species is HF, the organic material having a higher vapor pressure than water at standard conditions of room temperature and pressure of 1 atmosphere is methanol, thepressure is 300 Torr and the temperature is from 80.degree. C. to 95.degree. C.
8. A method of etching as claimed in claim 1 where the halide-containing species is HF, the low molecular weight organic molecule having a higher vapor pressure than water at standard conditions of room temperature and pressure of 1 atmosphereis methanol, the pressure is 500 Torr and the preset temperature is from 95.degree. C. to 105.degree. C.
9. A method of etching as claimed in claim 1 where the etching is performed in an enclosed chamber which is a reactor body of an apparatus further comprising:
a gas delivery system;
a UV source;
an IR source;
a rotating mechanism to rotate the wafer; and
a vacuum control system.
10. A method of etching as claimed in claim 1 where the organic material having a higher vapor pressure than water at standard conditions of room temperature and pressure of 1 atmosphere is anhydrous.
11. A method of etching as claimed in claim 1 where the halide-containing species is anhydrous.
12. A method of etching oxides on a surface of a substrate, said substrate being at a temperature of from 30.degree. C. to 70.degree. C., said method comprising etching with a gas phase mixture of HF and acetone, in an enclosed chamber at apressure of 500 Torr such that water is substantially maintained in the gas phase and condensation of species present on the etched surface is minimized. |
| Description: |
BACKGROUND OF THE INVENTION
The present invention relates to a method of etching oxides on a substrate to minimize or prevent deposition of contaminants on the substrate. In particular, the present invention relates to the etching of silicon oxides.
In integrated circuit manufacturing, the etching of oxides is typically carried out using a halide-containing water solution, for instance a HF/water solution, or reactive ion etching (RIE). The former method is not compatible with integratedprocessing of integrated circuits while the latter damages the surface of the substrate and contaminates the near-surface region of the substrate. As a result, neither method permits integration of oxide etching with other steps performed in a clusterprocessor.
The use of gaseous HF and water vapor, for example, is an alternative to RIE for gas-phase oxide etching. In this process, water vapor is needed to uniformly initiate etching. Gas phase etching can produce the same level of hydrogen terminationas the traditional HF/water rinse process. The process is well developed and is supported by commercial reactors. It works on the premise that the HF-water vapor mixture delivered to the oxide condenses there, and hence, the etching process iseventually taking place in the liquid phase. One of the problems encountered with this etching mode is that some of the reaction products may precipitate on the surface where they are difficult to remove without an additional deionized water rinse. Also, difficulties with precise control of the condensed liquid film composition and its uniform coverage of the oxide may, under certain conditions, result in inadequate etch uniformity and run-to-run reproducibility. Moreover, since existing HF vaporetch chemistry generally involves the addition of water vapor, the process is difficult to integrate with reduced pressure reactors and stainless steel components.
U.S. Pat. No. 5,022,961 to Izumi et al., incorporated herein by reference, implements an approach in which etching is performed using HF and alcohol where water added to the system is minimized. Etching is performed at room temperature andatmospheric pressure and liquid as well as vapor state etching are contemplated. Ionic contaminant, however, remains on the surface after etching, contained within the alcohol layer. After-treatment is again required to remove the contamination.
Prior art etching techniques suggest the use of particular solvent molecules for etching in certain circumstances. Izumi et al., for instance, discusses etching with HF or other halide-containing species only in combination with alcohol. Wetetching has prevalently been disclosed with HF, water and acetic acid alone or a mixture of organic acids. U.S. Pat. No. 4,746,397 to Maeda et al. does disclose etching with the use of a fluorine-containing species and an alcohol, ketone or carboxylicacid. However, liquid or vapor phase etching is contemplated under reduced pressure where the addition of water is specified.
It is disclosed in U.S. Pat. No. 4,857,142 to Syverson and U.S. Pat. No. 4,749,440 to Blackwood that etching may be accomplished with a minimum of added water where the oxide itself contains sufficient water. It is thus considered in the artthat at least some water is required for etching.
Drawbacks of prior practice are addressed by the present invention in a method of etching oxides on a surface of a substrate comprising etching at a preset wafer temperature with a gas phase mixture of a halide-containing species and a lowmolecular weight organic molecule having a high vapor pressure at standard conditions, in an enclosed chamber at a pressure such that all species present are substantially maintained in the gas phase and condensation of species present on the etchedsurfaces is controlled. Because trace water vapor may appear in the process chamber, water vapor is taken into account as a species present in the gas phase. Because water is less volatile than the constituent reactants, the temperature and pressureparameters are chosen from the area below the curve for water in the phase diagram. By maintaining temperature and pressure parameters within this range, all species present in the chamber, including water, are substantially maintained in the gas phase. Low molecular weight organic molecules having high vapor pressure at standard conditions encompass low molecular weight alcohols, organic acids, ketones or alkanes such as methanol, isopropanol, acetone, acetic acid and methane. Preferably, etching isperformed in a cluster dry tool apparatus. The process achieves controlled, gas-phase etching of oxides with etch rates up to two orders of magnitude lower than typical rates obtained for vapor HF/water etching, without the addition of water vapor tothe input gases.
The present invention also addresses drawbacks of prior practice by a method of etching oxides comprising etching with a halide-containing species and water where the pressure and temperature parameters are, as discussed above, selectively chosenfrom parameters below the curve representing water in the phase diagram.
It is an objective of the present invention to provide a method of etching oxides in which the oxide etch rate is controlled.
It is an objective of the present invention to provide a method of etching oxides in which condensation of species present on the etched surfaces is controlled.
It is a further objective of the present invention to provide a method which controls etch at a rate of up to two orders of magnitude lower than typical rates obtained for vapor HF/water etching.
SUMMARY OF THE INVENTION
The present invention provides a method of etching oxides on a surface of a substrate comprising etching at a preset wafer temperature with a gas phase mixture of a halide-containing species and a low molecular weight organic molecule having ahigh vapor pressure at standard conditions, in an enclosed chamber at a pressure such that all species present are substantially maintained in the gas phase and condensation of species present on the etched surfaces is controlled. Because trace watervapor may appear in the process chamber, water vapor is taken into account as a species present in the gas phase. Because water is less volatile than the constituent reactants, the temperature and pressure parameters are chosen from the area below thecurve for water in the phase diagram. By maintaining temperature and pressure parameters within this range, all species present in the chamber, including water, are substantially maintained in the gas phase. Low molecular weight organic moleculeshaving high vapor pressure at standard conditions encompass low molecular weight alcohols, organic acids, ketones or alkanes such as methanol, isopropanol, acetone, acetic acid and methane. Preferably, etching is performed in a cluster dry toolapparatus. The process achieves controlled, gas-phase etching of oxides with etch rates of up to two orders of magnitude lower than typical rates obtained for vapor HF/water etching, without the addition of water vapor to the input gases.
Alternatively, the present invention may be used with a halide-containing species and water, without the addition of a low molecular weight, high vapor pressure organic molecule where the pressure and temperature parameters are again selectivelychosen from parameters below the curve representing water in the phase diagram as discussed above.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a phase diagram representing vapor pressure of HF, methanol and water as a function of temperature.
FIG. 2 is a graph of oxide etch rates in HF/methanol at three different pressures as a function of wafer temperature.
FIG. 3 is a graph of oxide etch rate as a function of HF/methanol flow ratio.
FIG. 4 is a graph of XPS spectra for HF/methanol treated substances in accordance with the present invention.
FIG. 5 is a graph of oxide etched in HF/acetone as a function of temperature.
FIG. 6 is a graph of oxide etched in HF/acetone as a function of HF partial pressure.
DETAILED DESCRIPTION OF THE INVENTION
The gas-phase oxide etching method of the present invention involves the use of an agent effective in stimulating etching with gaseous HF as well as producing a hydrogen-terminated surface. Furthermore, the present invention involves thecreation of conditions under which the condensation of reactants and other contaminants on the oxide surface is either prevented, or more precisely controlled. The deposition of particulate contamination on the substrate surface, which would benonvolatalizable if deposited, is thus prevented.
Etching is carried out at temperatures and pressures at which condensation of reactants on the wafer surface can be effectively controlled. To assure adequate process reproducibility and control of the etch, temperature and pressure parameterswhich prevent condensation of the reactants and water on the etched surface are selected. Under the process conditions preventing condensation and eliminating moisture from interacting with etched surfaces, BPSG: thermal oxide etch selectivity in excessof 6000 is observed. Also, there is indirect evidence suggesting hydrogen termination of etched silicon surfaces.
Preferably, etching is performed with a gas phase mixture of a halide-containing species and a low molecular weight organic molecule having a high vapor pressure at standard conditions. It is here recognized that organic molecules having lowmolecular weight and high vapor pressure at standard conditions are generally applicable in the method of the present invention. These molecules include low molecular weight alcohols, organic acids, ketones or alkanes such as methanol, isopropanol,acetone, acetic acid and methane. In addition to their favorable solvent properties, these molecules are volatalizable. It is most preferable that the low molecular weight, high vapor pressure organic molecules be capable of removing any water whichmay be present on the oxide surface, particularly, for instance, when etching a BPSG oxide. Furthermore, it is most preferable that the organic molecule be capable of ionizing the halide-containing species which etches the oxide and generating Si-OHprecursor uniformly on the water surface. Such molecules which are most preferable include low molecular weight alcohols, organic acids and ketones such as methanol, isopropanol, acetone and acetic acid. Moreover, it has been recognized that suchmolecules actually initiate the etch when present with the halide-containing species. It is also believed that the presence of carbon in a low molecular weight, high vapor pressure molecule may be sufficient to stimulate the initiation of etching. Therefore, in a less preferred embodiment of the present invention, molecules which do not contain oxygen-bearing nucleophilic moieties yet are generally carbon containing organic molecules of low molecular weight and high vapor pressure at standardconditions, e.g., methane, may be utilized.
Halide-containing species include, in particular, HF, NF.sub.3, ClF.sub.3, F.sub.2 as well as other fluoride liberating species. Generally, the halide-containing species are compounds that readily crack with UV treatment in the presence of astimulant. Other examples of halide-containing species and low molecular weight, high vapor pressure organic molecules will be readily apparent to those skilled in the art.
The preferred aspect of the present invention focuses on the minimization of water present during the oxide etch. Therefore, it is preferred that either or both of the constituent reactant species be present in anhydrous form. Accordingly, inthe preferred embodiment a low molecular weight organic molecule having a high vapor pressure at standard conditions is utilized with a halide-containing species, without the addition of water to the input gases. In the most preferred embodiment,anhydrous forms of both of these constituent reactant species are present, without the addition of water.
The selection of process parameters is made on the basis of a phase diagram showing the variation of vapor pressures vs. temperature. Water is considered as it is the least volatile among the species present including halide-containing species,low molecular weight organic molecules having high vapor pressure at standard conditions and any water present. FIG. 1 is a phase diagram representing individual vapor pressure curves of HF, methanol and water as a function of temperature. As long asthe temperature and corresponding pressure of the oxide etching process are selected from the area below the curve for water as in FIG. 1, then all reactants involved should remain in the gas phase even if trace water vapor appears in the process chambereither as a product of the etching reaction, or in the input gases. In particular, where a surface of a substrate is at a preset temperature, etching is performed at a pressure such that all species present are substantially maintained in the gas phaseand condensation of species present on the etched surface is controlled.
In this manner FIG. 1 indicates, for instance, that at 100 Torr, all species present during HF/methanol etching should be in the vapor phase at 60.degree. C. and higher. At 300 Torr, all species present should be in the vapor phase at80.degree. C. and higher and at 500 Torr, the vapor phase should be achieved at 95.degree. C. and higher. Generally, FIG. 1 illustrates that as a higher pressure is chosen, the minimum range of temperatures which may be chosen is correspondinglyhigher. As a higher temperature is chosen, the maximum range of pressure which may be chosen increases, in order to maintain all species present in the gas phase.
The same may not apply to the etching of heavily hydrated oxides, such as borophosphosilicate glass (BPSG), where moisture contained in the etched oxide may not be driven from the surface fast enough to prevent fast etching. On the other hand,it is believed that increased temperature and reduced pressure will enhance vaporization of at least some reaction products, thereby reducing formation of solid residues on the etched surfaces.
In certain experiments, moisture has been driven from the oxide under vacuum conditions. Etching was then attempted with HF alone and with further addition of a low molecular weight organic molecule having a high vapor pressure at standardconditions. From these experiments it has been determined that in etching with a halide-containing species and a low molecular weight, high vapor pressure organic molecule, the low molecular weight, high vapor pressure organic molecule is responsiblefor initiation of the etch. Moreover, reactions of halide-containing species with water vapor and reactions of halide-containing species with low molecular weight, high vapor pressure organic molecules appear to be driven by different reactionmechanisms.
In a less preferred embodiment, the method of etching of the present invention is applicable to etching with a halide-containing species and water, without the use of a low molecular weight, high vapor pressure organic molecule. Similar to themethod described above, temperature and pressure parameters are selectively chosen such that all constituents remain in the gas phase.
One application for which the method of the present invention is well suited is etching of sacrificial oxide in a cluster tool or like environment immediately prior to gate oxidation. The cluster tool apparatus has been disclosed in U.S. Pat. No. 5,228,206 to Grant et al., which is incorporated herein by reference. The cluster tool module permits dry process cleaning according to the present invention on a commercial scale. It includes a 200 mm. wafer compatible reactor equipped with IRheating lamps and a vacuum control systems such as a dry mechanical pump and turbo pump allowing pressure reduction down to 10.sup.-6 Torr. To increase process uniformity, rotation of the wafer using a frictionless mechanism can be employed duringetching. A high purity halide-containing species is delivered from a nickel cylinder, and a gas delivery system or stainless steel bubbler is used to contain and supply liquid low molecular weight organic solvent having high vapor pressure at standardconditions, with nitrogen as a carrier gas. This gas delivery system permits the gas to pick up the vapor without liquid transport. The system uses an all stainless steel gas delivery system. Moreover, the UV lamp assists in driving off moleculeswhich may begin to condense, particularly after etching is complete and the species present are replaced with nitrogen gas. The use of the UV lamp markedly reduces processing time of the wafers.
The following examples demonstrate the applicability of HF/methanol and HF/acetone in the present invention. The present invention has also been observed to achieve similar results using ethanol as the low molecular weight, high vapor pressureorganic molecule, as the results set forth in Examples I and II using methanol and acetone. A brief experiment using HF/acetic acid further indicated that acetic acid is also applicable in the present invention. It has also been documented thatHF/isopropanol is applicable in the present invention and achieves analogous results to those shown for HF/methanol. See "Gas-Phase Etching of Silicon Oxide with Anhydrous HF and Isopropanol", Third Int'l Symposium on Cleaning Technology inSemiconductor Development Mfg., Subcommittee of Electrochemical Society, Oct. 15-20, 1993, citing Ruzyllo et al., J. Electrochem. Soc., 140:4, April, 1993, p. L64-L66.
EXAMPLE I
A prototype cluster tool compatible commercial apparatus was used. Special attention was given to the elimination of moisture and the prevention of reactant condensation in any part of the hardware upstream of the pressure control valve. Variation of process parameters included changes of pressure from 100 to 500 Torr, wafer temperature from 25.degree. to 110.degree. C., and CH.sub.3 OH carrier gas/HF gas flow ratio from 0 to 6. X-ray photoelectron spectroscopy (XPS) was used toevaluate the chemical condition of the silicon surface following etching.
Thermal oxides were grown in dry oxygen to the thickness of 1100 .ANG.. For each etching run, initial and final oxide thicknesses were determined using an automated ellipsometer with index of refraction n=1.465. For the sake of preliminaryevaluation of etch selectivity, the rates of BPSG etching under the conditions defined above were also determined. The BPSG films initially 6500 .ANG. thick were formed using a conventional chemical vapor deposition process.
The experimental portion was focused on: (i) establishing a correlation between oxide etch rates and pressure of anhydrous HF/CH.sub.3 OH/N.sub.2 mixture and wafer temperature, and (ii) determining the effect of methanol on the etch rates andchemical state of the Si surfaces.
Etching was performed with HF and methanol at various pressures and wafer temperatures. An IR pyrometer was used to determine wafer temperature. FIG. 2 presents the observed changes of thermal oxide etch rates in HF/methanol at three differentpressures as a function of wafer temperature. As seen in FIG. 2, etch rates decrease as wafer temperatures increase. Moreover, at higher pressures these changes are significantly more pronounced. In addition, the etch rates are much more reproducibleat temperatures which, at any given pressure, correspond to the etching regime assumed to be condensation-free. Thus the pressure and temperature parameters discussed above in regard to the phase diagram of FIG. 1 are shown to have the most controlledetch rate in FIG. 2. These effects are an indication that with increased wafer temperature, less condensation is gradually taking place and gas-phase reactions are becoming a dominant factor in the etching process. This behavior is reflected by theoxide etch rates up to two orders of magnitude lower than typical rates obtained for vapor HF/water etching. In the condensation-controlled etching regime identified in FIG. 2, variations of temperature and pressure can be used to control etch rates ofoxides from zero to about 200 .ANG./min.
Etching with HF/methanol was thus accomplished at a selectively chosen pressures of between 100 to 500 Torr and corresponding wafer temperatures of between 25.degree. to 120.degree. C. such that all species present are in the gas phase andcondensation of species present on the etched surfaces is controlled. In particular, gas phase etching with HF and methanol with a controlled etch was achieved at a preset temperature and at a pressure such that water is substantially maintained in thegas phase. As shown in FIG. 2, such parameters were demonstrated in the HF/methanol system at 100 Torr from 20.degree. C. to 95.degree. C.; at 300 Torr from 80.degree. to 95.degree. C.; and at 500 Torr from 95.degree. to 105.degree. C.
In the case of BPSG however, under the same process conditions the etch rates remain very high; typically etch rates in excess of 6000 .ANG./min were recorded which means that BPSG: thermal oxide etch selectivity in the range of thousands can beaccomplished. These high etch rates are believed to be due to the heavy hydration of BPSG resulting in significant enhancement of the etching reaction. At the temperatures and pressures applied in this experiment moisture contained in BPSG is notdriven away fast enough to prevent fast oxide etching.
In order to test the effect of methanol on the oxide etching in the condensation-controlled regime, moisture was driven from the oxide under vacuum conditions and the etch rates for various CH.sub.3 OH/HF ratios were determined. Surprisingly,the results shown in FIG. 3 clearly demonstrate that the methanol is responsible for initiating the etching process. An important data point shown is the apparent lack of any etching taking place at the CH.sub.3 OH/HF=0, i.e., during exposure of theoxide to gaseous HF only. This result indicates that methanol is the initiator of the etching reactions, and hence, that the controlled, effective etching of dry thermal oxide can be accomplished without the addition of water vapor to the input gases. The participation of moisture likely generated as a product of chemical reactions involved in etching does not change the fact that the mechanism of HF/CH.sub.3 OH etching appears to be different from vapor HF/H.sub.2 O etching. This notion is supportedby the comparison between predicted SIO.sub.2 etch rates for the HF/H.sub.2 O process at 25.degree. C. and 100 Torr with etch rates observed in this experiment at the same temperature and pressure. In this experiment etch rates are six to eight timeslower than predicted rates for vapor HF/H.sub.2 O etching, which indicates a different process etching mechanism for each.
The same HF.sub.2.sup.- species are likely responsible for oxide etching in the case of both vapor HF/water and HF/CH.sub.3 OH etching. Since the former is known to yield a mostly hydrogen-terminated silicon surface, one can expect the same inthe case of HF/CH.sub.3 OH etching. Two observations support this speculation. One is that silicon surfaces, from which the oxide was removed entirely using the HF/CH.sub.3 OH chemistry, display hydrophobic features as revealed through visualinspection of the behavior of water droplets on the etched surfaces. The second comes from the x-ray photoelectron spectroscopy (XPS) characterization of HF/CH.sub.3 OH treated surfaces.
FIG. 4 is a graph of XPS spectra for HF/methanol treated substances in accordance with the present invention. As XPS cannot detect hydrogen, weak F.sub.15 and O.sub.15 peaks may be an indication of a mostly hydrogen-terminated surface. In fact,the XPS spectrum in this case is strikingly similar to the one reported for a vapor HF/water treated silicon surface.
EXAMPLE II
The above experiments were performed under the same operating conditions, although utilizing HF/acetone rather than HF/methanol.
FIG. 5 is a graph of oxide etched in HF/acetone as a function of temperature at a pressure of 500 Torr. Flow rates were as follows: acetone at 300 standard cubic centimeters per minute (sccm); nitrogen at 425 sccm; and HF at 100 sccm. While notdepicting rate of etch v. temperature as in FIG. 2 regarding the use of HF/methanol, the results shown for HF/acetone are similar to those of HF/methanol. At 500 Torr a sharp increase in etch rate occurs with HF/acetone at lower temperatures, similar tothat observed for HF/methanol. At higher temperatures, above 30.degree. C., a slow, controlled etch rate is observed, similar to the rate observed at higher temperatures for HF/methanol.
As in Example I for HF/methanol, the gas phase oxide etching results with HF/acetone indicate that etching was achieved at a preset temperature and pressure such that all species present, including water, are substantially maintained in the gasphase and condensation of species present on the etched surfaces is controlled. Thus it appears from FIG. 5, that a controlled etch is obtained for HF/methanol at 500 Torr from about 30.degree. C. to 70.degree. C.
FIG. 6 is a graph of oxide etched in HF/acetone as a function of HF partial pressure at 500 Torr and 20.degree. C., with a total flow of 1000 sccm and an acetone flow of 364 sccm. The amount of oxide etched increases exponentially with HFpartial pressure. These results are also similar to those shown in FIG. 3 for etch rate v. HF/methanol flow ratio.
It will be understood that changes may be made in the above-described method without departing from the scope of the invention. It is accordingly intended that all matter contained in the above description or shown in the accompanying drawingsbe interpreted as illustrative rather than in a limiting sense.
It is also to be understood that the following claims are intended to cover all of the generic and specific features of the invention as described herein, and all statements of the scope of the invention which, as a matter of language, might besaid to fall therebetween.
* * * * * |
|
|
|
